EP3160975B1 - Transition metal catalysts for olefin polymerization - Google Patents
Transition metal catalysts for olefin polymerization Download PDFInfo
- Publication number
- EP3160975B1 EP3160975B1 EP15811109.6A EP15811109A EP3160975B1 EP 3160975 B1 EP3160975 B1 EP 3160975B1 EP 15811109 A EP15811109 A EP 15811109A EP 3160975 B1 EP3160975 B1 EP 3160975B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- alkyl
- aryl
- polar monomer
- transition metal
- heteroaryl
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 0 CP1(N(*)ICCN1*)=O Chemical compound CP1(N(*)ICCN1*)=O 0.000 description 19
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F210/00—Copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F210/02—Ethene
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07F—ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
- C07F9/00—Compounds containing elements of Groups 5 or 15 of the Periodic Table
- C07F9/02—Phosphorus compounds
- C07F9/28—Phosphorus compounds with one or more P—C bonds
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07F—ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
- C07F9/00—Compounds containing elements of Groups 5 or 15 of the Periodic Table
- C07F9/02—Phosphorus compounds
- C07F9/28—Phosphorus compounds with one or more P—C bonds
- C07F9/38—Phosphonic acids [RP(=O)(OH)2]; Thiophosphonic acids ; [RP(=X1)(X2H)2(X1, X2 are each independently O, S or Se)]
- C07F9/44—Amides thereof
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F216/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an alcohol, ether, aldehydo, ketonic, acetal or ketal radical
- C08F216/12—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an alcohol, ether, aldehydo, ketonic, acetal or ketal radical by an ether radical
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F220/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F220/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
- C08F220/02—Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F220/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
- C08F220/02—Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
- C08F220/04—Acids; Metal salts or ammonium salts thereof
- C08F220/06—Acrylic acid; Methacrylic acid; Metal salts or ammonium salts thereof
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F220/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
- C08F220/02—Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
- C08F220/10—Esters
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F220/00—Copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride ester, amide, imide or nitrile thereof
- C08F220/02—Monocarboxylic acids having less than ten carbon atoms; Derivatives thereof
- C08F220/42—Nitriles
- C08F220/44—Acrylonitrile
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F4/00—Polymerisation catalysts
- C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
- C08F4/44—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
- C08F4/60—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
- C08F4/70—Iron group metals, platinum group metals or compounds thereof
- C08F4/7001—Iron group metals, platinum group metals or compounds thereof the metallic compound containing a multidentate ligand, i.e. a ligand capable of donating two or more pairs of electrons to form a coordinate or ionic bond
- C08F4/7003—Bidentate ligand
- C08F4/7004—Neutral ligand
- C08F4/7014—PO
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F4/00—Polymerisation catalysts
- C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
- C08F4/72—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from metals not provided for in group C08F4/44
- C08F4/80—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from metals not provided for in group C08F4/44 selected from iron group metals or platinum group metals
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F2410/00—Features related to the catalyst preparation, the catalyst use or to the deactivation of the catalyst
- C08F2410/01—Additive used together with the catalyst, excluding compounds containing Al or B
Definitions
- the present invention relates to transition metal complexes and, in particular, to transition metal complexes operable for catalysis of olefin polymerization.
- Free radical olefin polymerization is well-known and commercially important.
- copolymerizations of ethylene with polar industrial monomers such as vinyl acetate and acrylic acid, are increasingly complex, requiring high temperature and exceedingly high pressures.
- polar industrial monomers such as vinyl acetate and acrylic acid
- processes intrinsically lack precise control over the resulting polymer architecture, polymer molecular weight and incorporation of polar monomer.
- coordination polymerization has been explored for potential controllable strategies for the synthesis of polyolefins having various functionalities derived from the incorporation of a polar monomer.
- Two dominant classes of transition metal catalysts have been developed to date for copolymerization of ethylene and industrial polar monomers.
- the first class encompasses group 10 complexes coordinated by an ⁇ -diimine ligand, commonly referred to Brookhart-type catalysts.
- the remaining class employs neutral palladium complexes coordinated by a phosphine sulfonate (Drent-type).
- Brookhart catalysts complex stability is limited for polymerizations conducted above room temperature. Even state-of-the-art Brookhart catalysts are persistent for only about 15 minutes at or above 90°C.
- Drent catalysts generally exhibit greater thermal stability, they typically produce low-molecular weight copolymers of ethylene and polar industrial monomers and/or turnover with poor rates. Therefore, new transition metal catalysts are required for the production of polar functionalized polyolefins.
- the present invention provides a method of polymerization as set out in the claims.
- a chelating phosphine-phosphonic diamide (PPDA) ligand is described herein for constructing transition metal complexes operable for catalysis of olefin polymerization, including copolymerization of ethylene with polar monomer.
- a PPDA ligand described herein is of Formula (I): wherein A is selected from the group consisting of alkyl, alkenyl, aryl and heteroaryl and wherein R 1 , R 2 , R 3 , R 4 , R 5 and R 6 are independently selected from the group consisting of alkyl, heteroalkyl, cycloalkyl, heterocycloalkyl, aryl, heteroaryl, alkyl-aryl and alkyl-heteroaryl, wherein R 1 and R 2 may optionally form a ring structure and any combination of R 3 , R 4 , R 5 and/or R 6 may optionally form a ring structure.
- Transition metal complexes are described herein incorporating the PPDA ligand of Formula (I). Such transition metal complexes, are suitable catalysts for copolymerization of ethylene with polar monomer.
- a transition metal complex described herein is of Formula (II): wherein M is a transition metal, A is selected from the group consisting of alkyl, alkenyl, aryl and heteroaryl and wherein R 1 , R 2 , R 3 , R 4 , R 5 and R 6 are independently selected from the group consisting of alkyl, heteroalkyl, cycloalkyl, heterocycloalkyl, aryl, heteroaryl, alkyl-aryl and alkyl-heteroaryl, wherein R 1 and R 2 may optionally form a ring structure and any combination of R 3 , R 4 , R 5 and/or R 6 may optionally form a ring structure and wherein R 7 is selected from the group consisting of alkyl and aryl and R 8 is
- a transition metal complex may be of Formula (III): wherein M is a transition metal, A is selected from the group consisting of alkyl, alkenyl, aryl and heteroaryl, and wherein R 1 , R 2 , R 3 , R 4 , R 5 and R 6 are independently selected from the group consisting of alkyl, heteroalkyl, cycloalkyl, heterocycloalkyl, aryl, heteroaryl, alkyl-aryl and alkyl-heteroaryl, wherein R 1 and R 2 may optionally form a ring structure and any combination of R 3 , R 4 , R 5 and/or R 6 may optionally form a ring structure and R 7 and R 8 are moieties of a chelating alkyl or aryl ligand, L, and wherein X - is a non-coordinating counter anion.
- R 7 is an alkyl or aryl moiety and R 8 is a
- the method of olefin copolymerization comprises providing a reaction mixture of olefin monomer, polar monomer and transition metal complex of Formula (II) and copolymerizing the olefin monomer with the polar monomer in the presence of the transition metal complex. Copolymerization of the olefin and polar monomers can proceed by insertion or coordination polymerization through the transition metal complex.
- suitable olefin monomer is ethylene or propylene and polar monomer is selected from acrylic acid, alkyl acrylic acids, alkyl acrylates, acetates, vinyl ethers, acrylamide, vinyl ethers and/or acrylonitrile.
- polar monomer can be incorporated in-chain as opposed to incorporation at terminating end(s) of the copolymer.
- a copolymer comprises olefin monomer and polar monomer, wherein greater than 50 percent of the polar monomer is positioned in-chain, and the copolymer has molecular weight (M w ) of at least 5,000 Da. In some embodiments, the copolymer has molecular weight of at least 10,000 Da or 20,000 Da.
- suitable olefin monomer can be ethylene or propylene and polar monomer is selected from acrylic acid, alkyl acrylic acids, alkyl acrylates, acetates, vinyl ethers, acrylamide and/or acrylonitrile.
- alkyl refers to a straight or branched saturated hydrocarbon group optionally substituted with one or more substituents.
- an alkyl can be C 1 - C 30 .
- alkenyl refers to a straight or branched chain hydrocarbon group having at least one carbon-carbon double bond and optionally substituted with one or more substituents.
- aryl refers to an aromatic monocyclic or multicyclic ring system optionally substituted with one or more ring substituents.
- an aromatic monocyclic or multicyclic ring system may be substituted with one or more of alkyl, alkenyl, alkoxy, heteroalkyl and/or heteroalkenyl.
- heteroaryl refers to an aromatic monocyclic or multicyclic ring system in which one or more of the ring atoms is an element other than carbon, such as nitrogen, oxygen and/or sulfur.
- the aromatic monocyclic or multicyclic ring system may further be substituted with one or more ring substituents, such as alkyl, alkenyl, alkoxy, heteroalkyl and/or heteroalkenyl.
- cycloalkyl refers to a non-aromatic, saturated mono- or multicyclic ring system optionally substituted with one or more ring substituents.
- heterocycloalkyl refers to a non-aromatic, saturated mono- or multicyclic ring system in which one or more of the atoms in the ring system is an element other than carbon, such as nitrogen, oxygen or sulfur, alone or in combination, and wherein the ring system is optionally substituted with one or more ring substituents.
- heteroalkyl refers to an alkyl moiety as defined above, having one or more carbon atoms in the chain, for example one, two or three carbon atoms, replaced with one or more heteroatoms, which may be the same or different, where the point of attachment to the remainder of the molecule is through a carbon atom of the heteroalkyl radical.
- alkoxy refers to the moiety RO-, where R is alkyl or alkenyl defined above.
- a chelating phosphine-phosphonic diamide (PPDA) ligand is described herein for constructing transition metal complexes operable for catalysis of olefin polymerization, including copolymerization of ethylene with polar monomer.
- PPDA phosphine-phosphonic diamide
- a PPDA ligand described herein is of Formula (I): wherein A is selected from the group consisting of alkyl, alkenyl, aryl and heteroaryl and wherein R 1 , R 2 , R 3 , R 4 , R 5 and R 6 are independently selected from the group consisting of alkyl, heteroalkyl, cycloalkyl, heterocycloalkyl, aryl, heteroaryl, alkyl-aryl and alkyl-heteroaryl, wherein R 1 and R 2 may optionally form a ring structure and any combination of R 3 , R 4 , R 5 and/or R 6 may optionally form a ring structure.
- A is selected from alkyl, alkenyl, aryl and heteroaryl.
- Figure 1 illustrates various alkyl, alkenyl, aryl and heteroaryl structures from which A can be selected according to some embodiments described herein.
- R 1 and R 2 are independently selected from the group consisting of alkyl, heteroalkyl, cycloalkyl, heterocycloalkyl, aryl, heteroaryl, alkyl-aryl and alkyl-heteroaryl, wherein R 1 and R 2 may optionally form a ring structure.
- aryl or heteroaryl of R 1 and/or R 2 are substituted with one or more ring substituents.
- substituents can include fluorinated alkyl, halide, alkoxy and heterocycloalkyl structures.
- the substituents can be positioned ortho and/or para on the ring.
- Figure 2 illustrates various substituted aryl and heteroaryl structures from which R 1 and/or R 2 can be independently selected according to some embodiments described herein. Additionally, R 1 and/or R 2 can be independently selected from alkyl, heteroalkyl and cycloalkyl.
- Figure 3 illustrates alkyl, heteroalkyl and cycloalkyl structures from which R 1 and/or R 2 can be independently chosen according to some embodiments described herein. Further, R 1 and R 2 may form a ring structure.
- Figure 4 illustrates ring structures formed by R 1 and R 2 according to some embodiments.
- R 2 , R 3 , R 4 , R 5 and R 6 are independently selected from the group consisting of alkyl, heteroalkyl, cycloalkyl, heterocycloalkyl, aryl, heteroaryl, alkyl-aryl and alkyl-heteroaryl.
- Figure 5 illustrates alkyl, heterocycloalkyl and alkyl-aryl structures from which R 2 , R 3 , R 4 , R 5 and/or R 6 can be independently selected according to some embodiments described herein. Additionally, any combination of R 3 , R 4 , R 5 and/or R 6 may optionally form a ring structure.
- Figure 6 illustrates ring structures formed by various combinations of R 3 , R 4 , R 5 and/or R 6 according to some embodiments.
- Transition metal complexes are described herein incorporating the PPDA ligand of Formula (I). Such transition metal complexes, are suitable catalysts for copolymerization of ethylene with polar monomer.
- a transition metal complex described herein is of Formula (II): wherein M is a transition metal, A is selected from the group consisting of alkyl, alkenyl, aryl and heteroaryl and wherein R 1 , R 2 , R 3 , R 4 , R 5 and R 6 are independently selected from the group consisting of alkyl, heteroalkyl, cycloalkyl, heterocycloalkyl, aryl, heteroaryl, alkyl-aryl and alkyl-heteroaryl, wherein R 1 and R 2 may optionally form a ring structure and any combination of R 3 , R 4 , R 5 and/or R 6 may optionally form a ring structure and wherein R 7 is selected from the group consisting of alkyl and aryl and R 8 is
- a transition metal complex may be of Formula (III): wherein M is a transition metal, A is selected from the group consisting of alkyl, alkenyl, aryl and heteroaryl, and wherein R 1 , R 2 , R 3 , R 4 , R 5 and R 6 are independently selected from the group consisting of alkyl, heteroalkyl, cycloalkyl, heterocycloalkyl, aryl, heteroaryl, alkyl-aryl and alkyl-heteroaryl, wherein R 1 and R 2 may optionally form a ring structure and any combination of R 3 , R 4 , R 5 and/or R 6 may optionally form a ring structure and R 7 and R 8 are moieties of a chelating alkyl or aryl ligand, L, and wherein X - is a non-coordinating counter anion.
- R 7 is an alkyl or aryl moiety and R 8 is a
- a and R 1 , R 2 , R 3 , R 4 , R 5 and R 6 can be selected from any of the structures illustrated in Figures 1-6 as described in Section I above.
- X - is a non-coordinating counter anion, which preferably exhibits suitable organic solvent solubility.
- Suitable non-coordinating counter anions can include borates and aluminates.
- X - is selected from the group consisting of [B[3,5-(CF 3 ) 2 C 6 H 3 ] 4 ] - also designated as [BAr F 4 ] - , [B(C 6 F 5 ) 4 ] - , Al[OC(CF 3 ) 3 ] 4 - , SbF 6 and PF 6 .
- M can be any transition metal not inconsistent with the objectives of the present invention.
- M is selected from Group 10 of the Periodic Table consisting of nickel, palladium and platinum.
- M can also be selected from earlier group(s) of transition metal elements. Examples 2 and 3 hereinbelow provide several transition metal complexes of Formulas (II) and (III) respectively wherein palladium is the transition metal.
- a method of olefin copolymerization comprises providing a reaction mixture of olefin monomer, polar monomer and transition metal complex of Formula (II) and copolymerizing the olefin monomer with the polar monomer in the presence of the transition metal complex. Copolymerization of the olefin and polar monomers can proceed by insertion or coordination polymerization through the transition metal complex.
- suitable olefin monomer is ethylene or propylene and polar monomer is selected from acrylic acid, alkyl acrylic acids, alkyl acrylates, alkenyl acetates, acrylamide, vinyl ethers and/or acrylonitrile.
- polar monomer can be incorporated in-chain as opposed to incorporation at terminating end(s) of the copolymer.
- transition metal complexes of Formula (II) can exhibit marked thermal stability often persisting for at least 24 hours at 100°C during polymerization of ethylene. Such thermal stability allows transition metal complexes described herein to provide homopolymers and copolymers of molecular weight in excess of 10,000 Da, a threshold generally allowing for desirable physical properties. In some embodiments, homopolymers and copolymers produced according to methods described herein have molecular weight of 10,000-250,000.
- Figure 7 is a plot of productivity versus time for homopolymerization of ethylene by a transition metal complex of Formula (II) according to one embodiment described herein. The transition metal complex is 18 described in the following Examples.
- a copolymer comprises olefin monomer and polar monomer, wherein greater than 50 percent of the polar monomer is positioned in-chain, and the copolymer has molecular weight (M w ) of at least 5,000 Da or at least 10,000 Da.
- M w molecular weight
- in-chain refers to distribution of the polar monomer along interior regions or positions of the polymeric chain, as opposed to incorporation of polar monomer at the ends of the polymeric chain. The ability to distribute polar monomer in-chain provides unique properties to the resultant copolymer. For example, in-chain distribution of polar monomer can provide the copolymer enhanced gas barrier properties.
- such copolymer can exhibit enhanced barrier properties to oxygen and/or other degradative gases, thereby enabling use of the copolymer in various gas barrier applications such as food packaging, barrier films for electronics and substrates for dye-sensitized photovoltaics and/or thin film transistors.
- in-chain distribution of polar monomer can enhance adhesion characteristics of the copolymer relative to polyolefins, such as LDPE and HDPE.
- Enhanced adhesion characteristics expand compatibility of the copolymer with a variety of materials including dyes and/or other polar polymeric species and coatings. Therefore, copolymer described herein can serve as a bulk structural material for various laminate and/or surface coated architectures without the requirement of special surface pretreatments, such as exposure to peroxide or plasma, to render the surface hydrophilic.
- In-chain polar monomer can also serve as locations for anchoring various species to the copolymer.
- various biological molecules including amino acids and peptides may be attached via exposed functional groups of the copolymer leading to biological molecule immobilization.
- in-chain polar monomer can permit copolymer described herein to serve as a compatibilizing agent for polymer blends.
- the copolymer can inhibit phase separation in a mixture of two or more immiscible polymeric species.
- copolymer having in-chain polar monomer has molecular weight selected from Table I: Table I - Copolymer Molecular Weight (M w ) Da ⁇ 20,000 ⁇ 30,000 ⁇ 40,000 ⁇ 50,000 ⁇ 100,000 10,000-200,000
- percentage of polar monomer of the copolymer incorporated in-chain can be selected from Table II. As provided in Table II, polar monomer, in some embodiments, is exclusively incorporated in-chain. Table II - Polar Monomer In-chain (%) ⁇ 60 ⁇ 70 ⁇ 80 ⁇ 90 ⁇ 95 ⁇ 99 100 50-100
- mol.% of polar monomer incorporated into the copolymer can be selected from Table III.
- suitable olefin monomer can be ethylene and/or propylene and polar monomer is selected from acrylic acid, alkyl acrylic acids, alkyl acrylates, acetates, acrylamide, vinyl ethers and/or acrylonitrile.
- entry compound R 1 R 2 yield (%) 1 1 i -C 3 H 7 CH 3 - a 2 2 2-(CH 3 O)C 6 H 4 CH 3 52 3 3 i -C 3 H 7 i -C 3 H 7 69 4 4 i -C 5 H 11 i -C 3 H 7 74 5 5 C 6 H 5 i -C 3 H 7 92 6 6 2-FC 6 H 4 i -C 3 H 7 15 7 7 2,6-F 2 C 6 H 3 i -C 3 H 7 35 8 8 2-(CH 3 O)C 6 H 4 i -C 3 H 7 75 9 9 2-furyl i -C 3 H 7 43 10 10 2-(CF 3 O)C 6 H 4 i -C 3 H 7 24 a Used directly without isolation.
- N,N,N',N'- tetraisopropyl phenylphosphonic diamide (0.65 g, 2.0 mmol) in THF (30 mL) was added tert- butyllithium (1.4 mL, 2.4 mmol, 1.7 M in pentane) at -78 °C. The mixture was then warmed to -30 °C and stirred for 3 h.
- Entry catalyst C 2 H 4 (bar) time (min) yield (g) activity [kg (mol Pd) -1 h -1 ] M w a (Da) ⁇ ( M w / M n ) a Me br b 1 11 (25) 30 60 7.14 2,900 5,200 1.8 0.5 2 c 12 (50) 30 30 1.53 4,600 37,000 5.1 21 3 12 (12.5) 30 15 0.95 3,100 160,000 2.0 n.d.
- H(OEt 2 ) 2 BAr 4 F and NiMe 2 py 2 were prepared according to literature procedure of Brookhart et al., Organometallics, 2003 11 (11) 3920 and Campora et al., J. Organomet. Chem., 2003, 683, 220 , respectively.
- ( 8 )NiBr 2 was first formed by stirring the PPDA ligand (8) of Example 2 with Ni(II)bromide ethylene glycol dimethyl ether complex, followed by evaporation of volatiles. 2-Mesitylmagnesium bromide solution (1M in THF, 0.23 mmol) was added to a THF solution of ( 8 )NiBr 2 (0.18 g, 0.23 mmol) at -78 °C. The mixture was then slowly warmed to room temperature and stirred for 1 h. The solvent was removed under vaccum. The residue was recrystallized from tolulene to give 25 as an orange solid (0.18 g, 93% yield).
- H(OEt 2 ) 2 BAr 4 F (0.25 g, 0.25 mmol) and PPDA ligand (0.11 g, 0.25 mmol) were dissolved in toluene (3 mL).
- the solution was added into a solution of NiMe 2 py 2 (0.068 g, 0.28 mmol) dissolved in toluene (3 mL).
- the dark red solution was filtered to remove black Ni 0 .
- the solvent was reduced and layered with pentane.
- the resulting dark brown oil was triturated three times with Et 2 O (5 mL) and dried to yield 27 as a light brown solid (0.27 g, 74%).
- N, N, N', N' -tetramethyl phenylphosphonic diamide (0.20 g, 0.94 mmol) in THF (20 mL) was added t -BuLi (0.72 mL, 1.22 mmol, 1.7 M in pentane) at 0 °C and stirred for 30 min.
- t -BuLi 0.72 mL, 1.22 mmol, 1.7 M in pentane
- a THF solution of bis(2,4-dimethoxyphenyl)bromophosphine (0.40 g, 1.0 mmol, 6.0 mL solution) was added to the reaction mixture and then warmed slowly to room temperature and stirred for 30 min.
- N, N, N', N' -tetramethyl 4-( N , N -dimethylaminophenyl)phosphonic diamide (0. 20 g, 0.78 mmol) in THF (20 mL) was added t -BuLi (0.6 mL, 1.0 mmol, 1.7 M in pentane) at 0 °C and stired for 30 min.
- a THF solution (5 mL) of bis(2,4-dimethoxyphenyl)bromophosphine (0.33 g, 0.86 mmol) was added to the reaction mixture and then warmed slowly to room temperature then stirred for 30 min.
- the desired product C2a (0.11 g, 25.1 % yield) was isolated as a 2:1 mixture with residual N, N, N', N' -tetramethyl 4 - ( N, N- dimethylaminophenyl)phosphonic diamide as a yellow solid after silica gel column chromatography with dichloromethane/MeOH (95:5) as eluent. This mixture was carried forward without further purification.
- a 450 mL stainless steel autoclave was dried in an oven at 120 °C, and then allowed to cool inside the dry box. After cooling, toluene (300 mL) and an aliquot of catalyst 27 stock solution (1.35 ⁇ mol) was added. The autoclave was then sealed, stirred in a heated oil bath. After the inner temperature reached 95 °C, the autoclave was charged with ethylene (30 bar) and stirred for 15 min. The autoclave exothermed to 117 °C. The reaction was then quenched by addition of MeOH. The mixture was filtered and washed with MeOH. The solids were dried under vacuum at 80 °C overnight to afford 19.20 g polyethylene.
- a 450 mL stainless steel autoclave was dried in an oven at 120 °C, and then allowed to cool inside the dry box. After cooling, toluene (300 mL), an aliquot of catalyst 27 stock solution (1.35 ⁇ mol) and MEHQ (0.25 g, 1500 equiv.) was added. The autoclave was then sealed, stirred in a heated oil bath. After the inner temperature reached 100 °C, the autoclave was charged with ethylene (30 bar) and stirred for 15 min. The reaction was then quenched by addition of MeOH. The mixture was filtered and washed with MeOH. The solids were dried under vacuum at 80 °C overnight to afford 10.42 g polyethylene.
- polymerization continued in the presence of the functional additives known to disrupt and/or preclude ethylene polymerization with prior transition metal catalysts.
- a 450 mL stainless steel autoclave was dried in an oven at 120 °C, and then allowed to cool inside the dry box. After cooling, toluene (300 mL) and an aliquot of catalyst 27 stock solution (1.35 ⁇ mol) was added. The autoclave was then sealed, stirred in a heated oil bath. After the inner temperature reached 100 °C, the autoclave was charged with ethylene (3.5 bar) and stirred for 15 min. The reaction was then quenched by addition of MeOH. The mixture was filtered and washed with MeOH. The solids were dried under vacuum at 80 °C overnight to afford polyethylene. The molecular weight and polydispersity were determined by size exclusion chromatography.
- a 25 mL stainless steel autoclave was dried in an oven at 120 °C, and then allowed to cool inside the dry box. After cooling, an aliquot of catalyst 27 stock solution (10 ⁇ mol) and butyl vinyl ether (1.94 mL, 15 mmol) were diluted with toluene to 15 mL. The autoclave was then sealed, stirred in a heated oil bath. The autoclave was charged with ethylene (30 bar), heated to 100 °C and stirred for 12 hours. The reaction was then quenched by addition of MeOH. The mixture was filtered and washed with MeOH.
- a 25 mL stainless steel autoclave was dried in an oven at 120 °C, and then allowed to cool inside the dry box. After cooling, toluene (10 mL) and 30 (1.25 ⁇ mol, 2.0 mg) was added. The autoclave was then sealed and stirred in a heated oil bath. After the inner temperature reached 100 °C, the autoclave was then charged with ethylene (30 bar) and stirred for 15 min. The reaction was then quenched by addition of MeOH. The mixture was filtered and washed with MeOH. The solids were dried under vacuum at 100 °C overnight to afford 0.52 g white solid. The molecular weight and polydispersity were determined by size exclusion chromatography. The extent of branching in the polymer backbone was determined by 1 H-NMR spectroscopy. The same procedure was repeated for 31.
- a 25 mL stainless steel autoclave was dried in an oven at 120 °C, and then allowed to cool inside the dry box. After cooling, toluene (12 mL) 30 (10.5 ⁇ mol, 17.0 mg) and methyl acrylate (3mL, 33.1mmol) was added. The autoclave was then sealed and stirred in a heated oil bath. After the inner temperature reached 100 °C, the autoclave was then charged with ethylene (30 bar) and stirred for 12 hrs. The reaction was then quenched by addition of MeOH. The mixture was filtered and washed with MeOH. The polymer was redissolved in 10 mL toluene and precipitated again by the addition of MeOH.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Polymers & Plastics (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Materials Engineering (AREA)
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Biochemistry (AREA)
- General Health & Medical Sciences (AREA)
- Molecular Biology (AREA)
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Description
- The present invention relates to transition metal complexes and, in particular, to transition metal complexes operable for catalysis of olefin polymerization.
- Free radical olefin polymerization is well-known and commercially important. However, copolymerizations of ethylene with polar industrial monomers, such as vinyl acetate and acrylic acid, are increasingly complex, requiring high temperature and exceedingly high pressures. Further, such processes intrinsically lack precise control over the resulting polymer architecture, polymer molecular weight and incorporation of polar monomer. In view of these deficiencies, coordination polymerization has been explored for potential controllable strategies for the synthesis of polyolefins having various functionalities derived from the incorporation of a polar monomer. Two dominant classes of transition metal catalysts have been developed to date for copolymerization of ethylene and industrial polar monomers. The first class encompasses
group 10 complexes coordinated by an α-diimine ligand, commonly referred to Brookhart-type catalysts. The remaining class employs neutral palladium complexes coordinated by a phosphine sulfonate (Drent-type). These two classes have persistent limitations. For Brookhart catalysts, complex stability is limited for polymerizations conducted above room temperature. Even state-of-the-art Brookhart catalysts are persistent for only about 15 minutes at or above 90°C. While Drent catalysts generally exhibit greater thermal stability, they typically produce low-molecular weight copolymers of ethylene and polar industrial monomers and/or turnover with poor rates. Therefore, new transition metal catalysts are required for the production of polar functionalized polyolefins. - The present invention provides a method of polymerization as set out in the claims.
- A chelating phosphine-phosphonic diamide (PPDA) ligand is described herein for constructing transition metal complexes operable for catalysis of olefin polymerization, including copolymerization of ethylene with polar monomer. A PPDA ligand described herein is of Formula (I):
wherein A is selected from the group consisting of alkyl, alkenyl, aryl and heteroaryl and wherein R1, R2, R3, R4, R5 and R6 are independently selected from the group consisting of alkyl, heteroalkyl, cycloalkyl, heterocycloalkyl, aryl, heteroaryl, alkyl-aryl and alkyl-heteroaryl, wherein R1 and R2 may optionally form a ring structure and any combination of R3, R4, R5 and/or R6 may optionally form a ring structure. - Transition metal complexes are described herein incorporating the PPDA ligand of Formula (I). Such transition metal complexes, are suitable catalysts for copolymerization of ethylene with polar monomer. In the presently claimed invention, a transition metal complex described herein is of Formula (II):
wherein M is a transition metal, A is selected from the group consisting of alkyl, alkenyl, aryl and heteroaryl and wherein R1, R2, R3, R4, R5 and R6 are independently selected from the group consisting of alkyl, heteroalkyl, cycloalkyl, heterocycloalkyl, aryl, heteroaryl, alkyl-aryl and alkyl-heteroaryl, wherein R1 and R2 may optionally form a ring structure and any combination of R3, R4, R5 and/or R6 may optionally form a ring structure and wherein R7 is selected from the group consisting of alkyl and aryl and R8 is selected from the group consisting of amine, heteroaryl, monophosphine, halo and sulfoxide and wherein X- is a non-coordinating counter anion. - Alternatively, and not claimed herein, a transition metal complex may be of Formula (III):
wherein M is a transition metal, A is selected from the group consisting of alkyl, alkenyl, aryl and heteroaryl, and wherein R1, R2, R3, R4, R5 and R6 are independently selected from the group consisting of alkyl, heteroalkyl, cycloalkyl, heterocycloalkyl, aryl, heteroaryl, alkyl-aryl and alkyl-heteroaryl, wherein R1 and R2 may optionally form a ring structure and any combination of R3, R4, R5 and/or R6 may optionally form a ring structure and R7 and R8 are moieties of a chelating alkyl or aryl ligand, L, and wherein X- is a non-coordinating counter anion. In some embodiments, for example, R7 is an alkyl or aryl moiety and R8 is a carbonyl or oxide moiety of ligand, L. - Methods of olefin copolymerization are described herein. The method of olefin copolymerization comprises providing a reaction mixture of olefin monomer, polar monomer and transition metal complex of Formula (II) and copolymerizing the olefin monomer with the polar monomer in the presence of the transition metal complex. Copolymerization of the olefin and polar monomers can proceed by insertion or coordination polymerization through the transition metal complex. In some embodiments, suitable olefin monomer is ethylene or propylene and polar monomer is selected from acrylic acid, alkyl acrylic acids, alkyl acrylates, acetates, vinyl ethers, acrylamide, vinyl ethers and/or acrylonitrile. Moreover, as described further herein, polar monomer can be incorporated in-chain as opposed to incorporation at terminating end(s) of the copolymer.
- Resultant copolymer compositions are described herein. For example, a copolymer comprises olefin monomer and polar monomer, wherein greater than 50 percent of the polar monomer is positioned in-chain, and the copolymer has molecular weight (Mw) of at least 5,000 Da. In some embodiments, the copolymer has molecular weight of at least 10,000 Da or 20,000 Da. As described herein, suitable olefin monomer can be ethylene or propylene and polar monomer is selected from acrylic acid, alkyl acrylic acids, alkyl acrylates, acetates, vinyl ethers, acrylamide and/or acrylonitrile.
- These and other embodiments are further described in the detailed description which follows.
-
-
Figure 1 illustrates chemical structures from which A of compounds described herein are selected according to some embodiments. -
Figure 2 illustrates aryl and heteroaryl chemical structures from which R1 and/or R2 of compounds described herein are independently selected according to some embodiments. -
Figure 3 illustrates alkyl, heteroalkyl and cycloalkyl chemical structures from which R1 and/or R2 of compounds described herein are independently selected according to some embodiments. -
Figure 4 illustrates ring or cyclized structures formed by the combination of R1 and R2 according to some embodiments described herein. -
Figure 5 illustrates alkyl, alkyl-aryl and heterocycloalkyl structures from which R3, R4, R5 and/or R6 are independently selected according to some embodiments. -
Figure 6 illustrates ring or cyclized structures formed by various combinations of R3, R4, R5 and/or R6 according to some embodiments. -
Figure 7 is a plot of productivity versus time for homopolymerization of ethylene by a transition metal complex of Formula (II) according to one embodiment described herein. - Embodiments described herein can be understood more readily by reference to the following detailed description and examples and their previous and following descriptions. Elements, apparatus and methods described herein, however, are not limited to the specific embodiments presented in the detailed description and examples. It should be recognized that these embodiments are merely illustrative of the principles of the present invention.
- The term "alkyl" as used herein, alone or in combination, refers to a straight or branched saturated hydrocarbon group optionally substituted with one or more substituents. For example, an alkyl can be C1 - C30.
- The term "alkenyl" as used herein, alone or in combination, refers to a straight or branched chain hydrocarbon group having at least one carbon-carbon double bond and optionally substituted with one or more substituents.
- The term "aryl" as used herein, alone or in combination, refers to an aromatic monocyclic or multicyclic ring system optionally substituted with one or more ring substituents. For example, an aromatic monocyclic or multicyclic ring system may be substituted with one or more of alkyl, alkenyl, alkoxy, heteroalkyl and/or heteroalkenyl.
- The term "heteroaryl" as used herein, alone or in combination, refers to an aromatic monocyclic or multicyclic ring system in which one or more of the ring atoms is an element other than carbon, such as nitrogen, oxygen and/or sulfur. The aromatic monocyclic or multicyclic ring system may further be substituted with one or more ring substituents, such as alkyl, alkenyl, alkoxy, heteroalkyl and/or heteroalkenyl.
- The term "cycloalkyl" as used herein, alone or in combination, refers to a non-aromatic, saturated mono- or multicyclic ring system optionally substituted with one or more ring substituents.
- The term "heterocycloalkyl" as used herein, alone or in combination, refers to a non-aromatic, saturated mono- or multicyclic ring system in which one or more of the atoms in the ring system is an element other than carbon, such as nitrogen, oxygen or sulfur, alone or in combination, and wherein the ring system is optionally substituted with one or more ring substituents.
- The term "heteroalkyl" as used herein, alone or in combination, refers to an alkyl moiety as defined above, having one or more carbon atoms in the chain, for example one, two or three carbon atoms, replaced with one or more heteroatoms, which may be the same or different, where the point of attachment to the remainder of the molecule is through a carbon atom of the heteroalkyl radical.
- The term "alkoxy" as used herein, alone or in combination, refers to the moiety RO-, where R is alkyl or alkenyl defined above.
- In one aspect, a chelating phosphine-phosphonic diamide (PPDA) ligand is described herein for constructing transition metal complexes operable for catalysis of olefin polymerization, including copolymerization of ethylene with polar monomer. A PPDA ligand described herein is of Formula (I):
wherein A is selected from the group consisting of alkyl, alkenyl, aryl and heteroaryl and wherein R1, R2, R3, R4, R5 and R6 are independently selected from the group consisting of alkyl, heteroalkyl, cycloalkyl, heterocycloalkyl, aryl, heteroaryl, alkyl-aryl and alkyl-heteroaryl, wherein R1 and R2 may optionally form a ring structure and any combination of R3, R4, R5 and/or R6 may optionally form a ring structure. - Turning now to specific substituents of the PPDA ligand, A is selected from alkyl, alkenyl, aryl and heteroaryl.
Figure 1 illustrates various alkyl, alkenyl, aryl and heteroaryl structures from which A can be selected according to some embodiments described herein. - Moreover, R1 and R2 are independently selected from the group consisting of alkyl, heteroalkyl, cycloalkyl, heterocycloalkyl, aryl, heteroaryl, alkyl-aryl and alkyl-heteroaryl, wherein R1 and R2 may optionally form a ring structure. In some embodiments, aryl or heteroaryl of R1 and/or R2 are substituted with one or more ring substituents. Such substituents can include fluorinated alkyl, halide, alkoxy and heterocycloalkyl structures. In some embodiments, the substituents can be positioned ortho and/or para on the ring.
Figure 2 illustrates various substituted aryl and heteroaryl structures from which R1 and/or R2 can be independently selected according to some embodiments described herein. Additionally, R1 and/or R2 can be independently selected from alkyl, heteroalkyl and cycloalkyl.Figure 3 illustrates alkyl, heteroalkyl and cycloalkyl structures from which R1 and/or R2 can be independently chosen according to some embodiments described herein. Further, R1 and R2 may form a ring structure.Figure 4 illustrates ring structures formed by R1 and R2 according to some embodiments. - As described herein, R2, R3, R4, R5 and R6 are independently selected from the group consisting of alkyl, heteroalkyl, cycloalkyl, heterocycloalkyl, aryl, heteroaryl, alkyl-aryl and alkyl-heteroaryl.
Figure 5 illustrates alkyl, heterocycloalkyl and alkyl-aryl structures from which R2, R3, R4, R5 and/or R6 can be independently selected according to some embodiments described herein. Additionally, any combination of R3, R4, R5 and/or R6 may optionally form a ring structure.Figure 6 illustrates ring structures formed by various combinations of R3, R4, R5 and/or R6 according to some embodiments. - Transition metal complexes are described herein incorporating the PPDA ligand of Formula (I). Such transition metal complexes, are suitable catalysts for copolymerization of ethylene with polar monomer. In the presently claimed invention, a transition metal complex described herein is of Formula (II):
wherein M is a transition metal, A is selected from the group consisting of alkyl, alkenyl, aryl and heteroaryl and wherein R1, R2, R3, R4, R5 and R6 are independently selected from the group consisting of alkyl, heteroalkyl, cycloalkyl, heterocycloalkyl, aryl, heteroaryl, alkyl-aryl and alkyl-heteroaryl, wherein R1 and R2 may optionally form a ring structure and any combination of R3, R4, R5 and/or R6 may optionally form a ring structure and wherein R7 is selected from the group consisting of alkyl and aryl and R8 is selected from the group consisting of amine, heteroaryl, monophosphine, halo and sulfoxide and wherein X- is a non-coordinating counter anion. - Alternatively, and not claimed herein, a transition metal complex may be of Formula (III):
wherein M is a transition metal, A is selected from the group consisting of alkyl, alkenyl, aryl and heteroaryl, and wherein R1, R2, R3, R4, R5 and R6 are independently selected from the group consisting of alkyl, heteroalkyl, cycloalkyl, heterocycloalkyl, aryl, heteroaryl, alkyl-aryl and alkyl-heteroaryl, wherein R1 and R2 may optionally form a ring structure and any combination of R3, R4, R5 and/or R6 may optionally form a ring structure and R7 and R8 are moieties of a chelating alkyl or aryl ligand, L, and wherein X- is a non-coordinating counter anion. In some embodiments, for example, R7 is an alkyl or aryl moiety and R8 is a carbonyl or oxide moiety of ligand, L. - In some embodiments, A and R1, R2, R3, R4, R5 and R6 can be selected from any of the structures illustrated in
Figures 1-6 as described in Section I above. Further, X- is a non-coordinating counter anion, which preferably exhibits suitable organic solvent solubility. Suitable non-coordinating counter anions can include borates and aluminates. In some embodiments, for example, X- is selected from the group consisting of [B[3,5-(CF3)2C6H3]4]- also designated as [BArF 4]-, [B(C6F5)4]- , Al[OC(CF3)3]4 -, SbF6 and PF6. - M can be any transition metal not inconsistent with the objectives of the present invention. For example, in some embodiments, M is selected from
Group 10 of the Periodic Table consisting of nickel, palladium and platinum. However, M can also be selected from earlier group(s) of transition metal elements. Examples 2 and 3 hereinbelow provide several transition metal complexes of Formulas (II) and (III) respectively wherein palladium is the transition metal. - Methods of olefin copolymerization are described herein. A method of olefin copolymerization comprises providing a reaction mixture of olefin monomer, polar monomer and transition metal complex of Formula (II) and copolymerizing the olefin monomer with the polar monomer in the presence of the transition metal complex. Copolymerization of the olefin and polar monomers can proceed by insertion or coordination polymerization through the transition metal complex. In some embodiments, suitable olefin monomer is ethylene or propylene and polar monomer is selected from acrylic acid, alkyl acrylic acids, alkyl acrylates, alkenyl acetates, acrylamide, vinyl ethers and/or acrylonitrile. Moreover, as described further below with reference to Table II, polar monomer can be incorporated in-chain as opposed to incorporation at terminating end(s) of the copolymer.
- Importantly, transition metal complexes of Formula (II) can exhibit marked thermal stability often persisting for at least 24 hours at 100°C during polymerization of ethylene. Such thermal stability allows transition metal complexes described herein to provide homopolymers and copolymers of molecular weight in excess of 10,000 Da, a threshold generally allowing for desirable physical properties. In some embodiments, homopolymers and copolymers produced according to methods described herein have molecular weight of 10,000-250,000.
Figure 7 , for example, is a plot of productivity versus time for homopolymerization of ethylene by a transition metal complex of Formula (II) according to one embodiment described herein. The transition metal complex is 18 described in the following Examples. - Additionally, copolymer compositions are described herein. For example, a copolymer comprises olefin monomer and polar monomer, wherein greater than 50 percent of the polar monomer is positioned in-chain, and the copolymer has molecular weight (Mw) of at least 5,000 Da or at least 10,000 Da. As used herein, "in-chain" refers to distribution of the polar monomer along interior regions or positions of the polymeric chain, as opposed to incorporation of polar monomer at the ends of the polymeric chain. The ability to distribute polar monomer in-chain provides unique properties to the resultant copolymer. For example, in-chain distribution of polar monomer can provide the copolymer enhanced gas barrier properties. In some embodiments, such copolymer can exhibit enhanced barrier properties to oxygen and/or other degradative gases, thereby enabling use of the copolymer in various gas barrier applications such as food packaging, barrier films for electronics and substrates for dye-sensitized photovoltaics and/or thin film transistors.
- Moreover, in-chain distribution of polar monomer can enhance adhesion characteristics of the copolymer relative to polyolefins, such as LDPE and HDPE. Enhanced adhesion characteristics expand compatibility of the copolymer with a variety of materials including dyes and/or other polar polymeric species and coatings. Therefore, copolymer described herein can serve as a bulk structural material for various laminate and/or surface coated architectures without the requirement of special surface pretreatments, such as exposure to peroxide or plasma, to render the surface hydrophilic. In-chain polar monomer can also serve as locations for anchoring various species to the copolymer. For example, various biological molecules including amino acids and peptides may be attached via exposed functional groups of the copolymer leading to biological molecule immobilization. In additional aspect, in-chain polar monomer can permit copolymer described herein to serve as a compatibilizing agent for polymer blends. In some embodiments, the copolymer can inhibit phase separation in a mixture of two or more immiscible polymeric species.
- In some embodiments, copolymer having in-chain polar monomer has molecular weight selected from Table I:
Table I - Copolymer Molecular Weight (Mw) Da ≥ 20,000 ≥ 30,000 ≥ 40,000 ≥ 50,000 ≥ 100,000 10,000-200,000 - Additionally, percentage of polar monomer of the copolymer incorporated in-chain can be selected from Table II. As provided in Table II, polar monomer, in some embodiments, is exclusively incorporated in-chain.
Table II - Polar Monomer In-chain (%) ≥ 60 ≥ 70 ≥ 80 ≥ 90 ≥ 95 ≥ 99 100 50-100 - Further, mol.% of polar monomer incorporated into the copolymer can be selected from Table III.
Table III - mol.% Polar Monomer Incorporated into Copolymer 0.5-15 3-15 3-10 3-8 5-15 5-10 10-15 - As described herein, suitable olefin monomer can be ethylene and/or propylene and polar monomer is selected from acrylic acid, alkyl acrylic acids, alkyl acrylates, acetates, acrylamide, vinyl ethers and/or acrylonitrile.
- These and other embodiments are further illustrated by the following non-limiting examples.
-
- Representative synthesis of a PPDA ligand: N,N,N',N'-tetraisopropyl 2-[bis(2-methoxyphenyl) phosphino]phenylphosphonic diamide (8). To a solution of N,N,N',N'-tetraisopropyl phenylphosphonic diamide (0.65 g, 2.0 mmol) in THF (30 mL) was added tert-butyllithium (1.4 mL, 2.4 mmol, 1.7 M in pentane) at -78 °C. The mixture was then warmed to -30 °C and stirred for 3 h. A THF solution of bis(2-methoxyphenyl)chlorophosphine (0.84 g, 3.0 mmol) was added to the reaction mixture and then stirred for 30 min after slowly warming to room temperature. Evaporation of solvent and purification of the residue by column chromatography (ethyl acetate/hexane) gave 0.85 g (75 %) of 8 as a white solid. 1H NMR (500 MHz, CDCl3) δ 7.85 (ddd, J = 11, 7, 4 Hz, 1H), 7.32 (td, J = 7, 3 Hz, 1H), 7.26 (t, J = 11 Hz, 3H), 7.07 (dt, J = 7, 3 Hz, 1H), 6.85 (dd, J = 8, 4 Hz, 2H), 6.78 (t, J = 7 Hz, 2H), 6.60 (s, 2H), 3.78-3.65 (m, 10H), 1.32 (d, J = 7 Hz, 12H), 1.23 (d, J = 7 Hz, 12H). 31P NMR (121 MHz, CDCl3) δ 29.5, -25.8. 13C NMR (125 MHz, CDCl3) δ 160.9, 143.7, 140.2, 135.5, 134.2, 133.2, 130.1, 129.0, 128.1, 126.5, 120.5, 110.0, 55.2, 46.6, 24.2. HRMS (ESI) m/z Calc'd for C32H46N2O3P2+H (M+H) 569.3062, Found 569.3094.
- Compound 2 was prepared in an analogous way as for 8; 0.65 g (52%) of 2 was obtained as a white solid. 1H NMR (500 MHz, CDCl3) δ 8.24 (ddd, J = 11, 8, 3Hz, 1H), 7.44 (td, J = 7, 3Hz, 1H), 7.37 - 7.27 (m, 3H), 7.06 (d, J = 7 Hz, 1H), 6.88 (d, J = 8 Hz, 2H), 6.83 (td, J = 7, 3 Hz, 2H), 6.56 (s, 2H), 3.68 (s, 6H), 2.70 - 2.34 (m, 12H). 31P NMR (203 MHz, CDCl3) δ 30.9, -27.7. 13C NMR (126 MHz, CDCl3) δ 160.9, 141.3, 137.4, 136.0, 135.1, 134.1, 131.2, 129.9, 128.4, 125.6, 121.0, 109.9, 55.4, 36.8. HRMS (ESI) m/z Calc'd for C24H30N2O3P2+H (M+H) 457.1810, Found 457.1802.
-
- Representative synthesis of a (PPDA)palladium catalyst: [(8-k-P,k-O)(methyl)(2,6-lutidine)palladium] {tetrakis[3,5-bis(trifluoromethyl)phenyl]borate} (18). (1,5-cyclooctadiene)(chloro)(methyl)palladium (178 mg, 0.67 mmol) and 8 (381 mg, 0.67 mol) were weighed into a small vial. The mixture was dissolved in dichloromethane (5 mL) at room temperature, and the solution was stirred for 10 min. The total volume was reduced to ca. 2 mL under reduced pressure and then diluted with toluene (10 mL). After standing overnight, the mother liquor was decanted, the solids were washed with toluene and pentane then dried under vacuum to afford 409 mg of (8-k-P,k-O)(chloro)(methyl)palladium.
- (8-k-P,k-O)(chloro)(methyl)palladium (80 mg, 0.11 mmol) and 2,6-lutidine (13mg, 0.12 mmol) were weighed into a small vial and dissolved in dichloromethane (5 mL). The solution was then added to a flask containing sodium tetrakis[3,5-bis(trifluoromethyl)phenyl]borate (98 mg, 0.11 mmol) cooled to -78 °C. The mixture was slowly warmed to rt with vigorous stirring. Stirring was continued for an additional 30 min at rt. The solids were removed by filtration through Celite, the filtrate was concentrated to ca. 2 mL, and then diluted with toluene (10 mL). After standing overnight, the precipitate was filtered and washed with pentane then dried under vacuum to afford 119 mg (65%) of 18 as a pale yellow solid. 1H NMR (500 MHz, CD2Cl2) δ 8.68 (dd, J = 16, 8 Hz, 1H), 7.90 (ddd, J = 15, 8, 5 Hz, 1H), 7.82 (s, 8H), 7.71 (dd, J = 15, 10 Hz, 2H), 7.67- 7.60 (m, 6H), 7.52 (t, J = 8 Hz, 1H), 7.35- 7.22 (m, 4H), 7.12 (dd, J = 8, 6 Hz, 1H), 7.06- 6.97 (m, 2H), 6.77 (dd, J = 12, 8 Hz, 1H), 3.78 (s, 3H), 3.70-3.61 (m, 2H), 3.53 (s, 3H), 3.49- 3.41 (m, 2H), 3.31 (s, 3H), 3.18 (s, 3H), 1.16 (d, J = 7 Hz, 6H), 1.05 (d, J = 7 Hz, 6H), 1.02(d, J = 7 Hz, 6H), 0.93 (d, J = 7 Hz, 6H), 0.00 (d, J = 3 Hz, 3H). 31P NMR (121 MHz, CD2Cl2) δ 30.2, 24.9. 19F NMR (300 MHz, CD2Cl2) δ -62.9. 13C NMR (125 MHz, CD2Cl2) δ 161.7, 159.2, 158.6, 140.6, 138.5, 137.8, 136.8, 136.6, 135.0, 134.8, 134.0, 133.6, 133.0, 129.9, 129.3, 129.2, 128.9, 128.8, 125.2, 124.6, 122.7, 121.3, 120.6, 117.4, 116.0, 115.3, 111.7, 111.1, 54.9, 47.5, 47.3, 26.4, 24.2, 23.6, 22.7, 22.1, -2.8.
-
- Representative synthesis of a (PPDA)palladium catalyst: {(8-k-P,k-O){2-[(acetyl-k-O) amino]phenyl-kC} palladium}{tetrakis[3,5-bis(trifluoromethyl)phenyl]borate} (24). Bis[µ-(chloro)]bis[2-[(acetyl-k-O)amino]phenyl-k-C]dipalladium (111 mg, 0.40 mmol) and 8 (228 mg, 0.40 mmol) were weighed into a vial and CH2Cl2 (5 mL) was then added. The suspension was stirred at room temperature for 3 h. The solution was filtered through Celite, the filtrate was concentrated to ca. 2 mL, and the solution was diluted with toluene (10 mL). After standing overnight, the precipitate was filtered, washed with pentane, and then dried under vacuum to afford 241 mg of (8-k-P,k-O)[2-(N-acetylamino)phenyl](chloro)palladium as a yellow solid.
- (8-k-P,k-O)[2-(N-acetylamino)phenyl](chloro)palladium (137 mg, 0.16 mmol) was dissolved in CH2Cl2 (5 mL) and the solution was added to a flask containing AgSbF6 (56 mg, 0.16 mmol) cooled to -78 °C. The mixture was slowly warmed to room temperature over 30 min. The solids were removed by filtration through Celite, the filtrate was concentrated to ca. 2 mL, and the solution was diluted with toluene (10 mL). After standing overnight, the precipitate was filtered, washed with pentane, and dried under vacuum to afford 135 mg of {(8-k-P,k-O)[2-[(acetyl-k-O) amino]phenyl-k-C]palladium} {SbF6} as a yellow solid.
- {(8-k-P,k-O)[2-[(acetyl-k-O)amino]phenyl-k-C]palladium} {SbF6} (74 mg, 0.069 mmol) and sodium tetrakis[3,5-bis(trifluoromethyl)phenyl]borate (62 mg, 0.069 mmol) were weighed into a vial. CH2Cl2 (5 mL) was then added, and the mixture was stirred for 15 min. The solids were removed by filtration through Celite, the filtrate was concentrated to ca. 2 mL, and then diluted with pentane (10 mL). After standing overnight, the precipitate was filtered, washed with pentane, and dried under vacuum to afford 102 mg (88%) of 24 as a yellow solid. 1H NMR (500 MHz, CD2Cl2) δ 8.77 (s, 1H), 7.86 (s, 1H), 7.71- 7.62 (m, 1H), 7.58 (s, 8H), 7.48 (t, J = 8 Hz, 1H), 7.42 (s, 4H), 7.40- 7.30 (m, 2H), 7.29- 7.17 (m, 2H), 7.12- 7.05 (m, 1H), 6.82- 6.72 (m, 2H), 6.67 (d, J = 8 Hz, 1H), 6.55 (t, J = 8 Hz, 1H), 6.48- 6.40 (m, 1H), 6.38 (dd, J = 8, 2 Hz, 1H), 6.26 (t, J = 8 Hz, 1H), 5.99 (t, J = 8 Hz, 1H), 3.64- 3.49 (m, 2H), 3.47- 3.21 (m, 5H), 3.17 (s, 3H), 2.21 (s, 3H), 1.25 (d, J = 7 Hz, 6H), 1.01(d, J = 7 Hz, 6H), 0.98(d, J = 7 Hz, 6H), 0.73 (d, J = 7 Hz, 6H). 31P NMR (203 MHz, CD2Cl2) δ 30.9, 28.3. 13C NMR (125 MHz, CD2Cl2) δ 169.4, 161.8, 141.1, 140.0, 137.2, 136.7, 136.6, 136.0, 159.6, 134.7, 133.8, 133.5, 133.1, 132.6, 132.2, 130.5, 130.4, 129.7, 129.6, 128.8, 127.5, 124.63, 124.58, 123.8, 121.8, 120.7, 117.5, 115.0, 112.1, 111.4, 54.8, 47.8, 47.5, 23.7, 22.5, 22.1, 22.0.
-
Entry catalyst (mM) C2H4 (bar) time (min) yield (g) activity [kg (mol Pd)-1 h-1] M w a (Da) Ð (M w/M n)a Me brb 1 11(25) 30 60 7.14 2,900 5,200 1.8 0.5 2c 12 (50) 30 30 1.53 4,600 37,000 5.1 21 3 12 (12.5) 30 15 0.95 3,100 160,000 2.0 n.d.d 4 12 (25) 30 15 3.60 5,800 120,000 1.6 1.4 5 12 (25) 15 30 3.56 2,800 130,000 1.6 2.9 6 12 (25) 7 30 2.48 2,000 100,000 1.5 2.7 7 12 (25) 3.5 30 1.19 950 21,000 2.5 7.0 8 13 (25) 30 15 1.08 1,700 39,000 1.6 2.5 9 14 (25) 23 30 2.60 1,000 81,000 1.4 16 10 15 (25) 30 30 trace - - - - 11 16 (25) 30 60 4.80 1,900 88,000 1.5 n.d.d 12 17 (25) 30 15 6.30 10,000 80,000 1.8 3.0 13c 18 (50) 30 30 1.74 5,700 26,000 5.7 n.d.d 14 18 (25) 30 15 1.35 2,200 240,000 1.4 13 15 18 (25) 3.5 120 1.35 270 16,000 1.6 21 16 19 (25) 30 60 1.45 580 1,400 1.7 n.d.d 17 20 (25) 30 30 trace - - - - 18 24 (25) 30 30 0.19 160 160,000 1.3 n.d.d 19 30 (12.5) 30 15 0.52 1,700 140,000 1.3 4 20 31 (12.5) 30 15 2.12 6,800 120,000 1.4 7 aAbsolute molecular weight and polydispersity determined by GPC analysis with triple detection. bMethyl branches per 1000 carbons as determined by 1H or quantitative 13C NMR spectroscopy.. cReaction conducted in a 7-well autoclave; 10 mL total volume. dNot determined. -
Entry catalyst (mM) R (M) time (h) yield (g) activity [kg (mol Pd)-1 h-1] M w a (Da) Ð (M w/M n) Me brb Cc (%) 1 12 (0.67) CO2H (1.5) 15 0.66 4.4 31,000 2.9 1.2 2.7 2d 12 (0.67) CO2Me (2.2) 12 0.27 2.2 21,000 1.4 7.4 2.0 3 12 (0.67) CO2Me (2.2) 15 1.48 9.9 74,000 1.6 2.1 0.7 4 17 (0.67) CO2Me (2.2) 9 0.83 9.2 9,100 3.5 n.d.e n.d.e 5 18 (0.67) CO2Me (2.2) 13 0.32 2.4 29,000 1.4 4.8 1.3 6 23 (0.69) CH2OAc (1.6) 15 0.97 6.2 23,000 2.1 2.5 1.0 7 12 (0.67) CH2OAc (1.6) 12 0.79 6.6 4,900 4.5 n.d.e 1.2 8 17 (0.67) CO2Me (2.2) 9 0.83 9.2 9,000 3.5 4.7 1.8 9 f 30 (0.70) CO2Me (2.2) 12 1.03 8.3 19,000 1.5 n.d.e 3.7 10f 31 (0.86) CO2Me (2.2) 12 4.11 26 34,000 1.8 n.d.e 8.6 aAbsolute molecular weight and polydispersity determined by GPC analysis with triple detection. bMethyl branches per 1000 carbons as determined by 1H NMR spectroscopy. cMole fraction of polar monomer incorporated into the product as determined by 1H NMR spectroscopy. d95 °C. eNot determined. f100 °C - Representative procedure for polymerizations: Reaction of ethylene and 18. A 450 mL stainless steel autoclave was dried in an oven at 120 °C, and then allowed to cool inside a dry box. After cooling, 4.2 mg (0.0025 mmol) of 18 was added and diluted with toluene (100 mL). The autoclave was sealed, equilibrated to 100 °C, and then charged with ethylene (30 bar). After 15 min, the autoclave was vented and the reaction was quenched by addition of MeOH. The solids were filtered, washed with MeOH, and dried under vacuum at 70 °C overnight. The molecular weight and polydispersity were determined by size exclusion chromatography. The extent of branching in the polymer backbone was determined by 1H NMR spectroscopy at 120 °C in CDCl2CDCl2.
- H(OEt2)2BAr4 F and NiMe2py2 were prepared according to literature procedure of Brookhart et al., Organometallics, 2003 11 (11) 3920 and Campora et al., J. Organomet. Chem., 2003, 683, 220, respectively.
-
- (8)NiBr2 was first formed by stirring the PPDA ligand (8) of Example 2 with Ni(II)bromide ethylene glycol dimethyl ether complex, followed by evaporation of volatiles. 2-Mesitylmagnesium bromide solution (1M in THF, 0.23 mmol) was added to a THF solution of (8)NiBr2 (0.18 g, 0.23 mmol) at -78 °C. The mixture was then slowly warmed to room temperature and stirred for 1 h. The solvent was removed under vaccum. The residue was recrystallized from tolulene to give 25 as an orange solid (0.18 g, 93% yield).
1H NMR (500 MHz, CD2Cl2) δ 7.83- 7.01 (m, 10H), 6.54 (br, 2H), 5.80 (br, 2H), 3.75 (br, 4H), 3.40 (br, 6H), 2.93 (br, 6H), 2.33 (br, 3H), 1.18 (br, 24H).
13C NMR (125 MHz, CD2Cl2) δ 160.44 , 141.42 , 136.34 (d, J = 12.8 Hz), 135.38, 135.16 (d, J = 9.9 Hz), 134.06 (d, J = 15.2 Hz), 132.43 (d, J = 8.5 Hz), 131.81 (dd, J = 36.1, 5.1 Hz), 129.96 , 129.22, 128.75 (d, J = 5.7 Hz), 128.41, 128.31, 127.03, 125.49, 123.97, 120.41, 110.11, 47.70 (d, J = 6.1 Hz), 27.15, 24.36, 23.86, 19.64.
31P NMR (203 MHz, CD2Cl2) δ 29.7 (d, J = 11.2 Hz), 11.65 (d, J = 11.6 Hz). -
- NaBArF 4 (71 mg, 0.080 mmol) in CH2Cl2 was added to a CH2Cl2 solution of 25 (66 mg, 0.080 mmol) and DMSO (24 mg, 0.32 mmol). After stirred at room temperature for 1 h, the solvent was removed and the residue was recrystallized from toluene and CH2Cl2 to give 26 as an a orange solid (80 mg, 59% yield).
1H NMR (500 MHz, CD2Cl2) δ 7.77 (br, 11H), 7.61 (br, 4H), 7.55- 7.40 (m, 5H), 7.05 (br, 2H), 6.62 (br, 2H), 6.01 (br, 2H), 3.87 - 3.65 (m, 4H), 3.44 (br, 6H), 3.16 - 2.77 (m, 6H), 2.41 - 2.22 (m, 6H), 1.95 (br, 3H), 1.19 (br, 24H).
13C NMR (125 MHz, CD2Cl2) δ 162.26 (q, J = 49.8 Hz), 160.60 , 143.12 , 136.32 (dd, J = 12.4, 2.4 Hz), 135.31 , 135.06 (d, J= 4.9 Hz), 134.18 (d, J= 10.5 Hz), 134.04 (d, J= 4.5 Hz), 133.72 (d, J = 9.4 Hz), 133.47 , 132.80 (t, J = 9.1 Hz), 129.87 (dd, J = 7.1, 2.8 Hz), 129.66 (d, J = 2.3 Hz), 129.38 (qq, J = 31.5, 2.9 Hz), 125.76, 125.11 (q, J = 272.3 Hz), 120.81 (d, J = 11.7 Hz), 118.00 (p, J = 4.3 Hz), 116.52, 116.08, 110.89 , 54.71 , 48.14 (d, J = 6.0 Hz), 38.54 , 26.40 , 24.19 (dd, J = 44.2, 3.3 Hz), 20.05.
31P NMR (203 MHz, CD2Cl2) δ 32.31 (d, J = 10.9 Hz), 16.71 (d, J = 11.2 Hz). HRMS (ESI) m/z calc'd for C41H57N2NiO3P2 (M+-DMSO) 745.3198, found 745.3199. -
- H(OEt2)2BAr4 F (0.25 g, 0.25 mmol) and PPDA ligand (0.11 g, 0.25 mmol) were dissolved in toluene (3 mL). The solution was added into a solution of NiMe2py2 (0.068 g, 0.28 mmol) dissolved in toluene (3 mL). After stirring for 4 hours, the dark red solution was filtered to remove black Ni0. The solvent was reduced and layered with pentane. The resulting dark brown oil was triturated three times with Et2O (5 mL) and dried to yield 27 as a light brown solid (0.27 g, 74%).
1H NMR (500 MHz, CD2Cl2) δH 8.74 (br, 2H), 7.79-8.0 (br, 6H), 7.72 (s, 8H), 7.56 (s, 4H), 7.31-7.51 (br, 5H), 7.05 (br, 4H), 3.80 (s, 6H), 2.27 (d, J= 10 Hz, 12H), -0.95 (d, J= 10 Hz, 3H).
13C NMR (125 MHz, CD2Cl2) δC 161.70 (q, J = 50 Hz), 160.65, 149.83, 147.20, 137.92, 135.98, 135.17 (d, J = 12 Hz), 134.72, 133.557, 132.69, 131.73 (d, J = 50 Hz), 130.17 (d, J = 11 Hz), 128.83 (d, J = 32 Hz), 126.91, 125.64, 124.76, 123.47, 121.00 (d, J = 9Hz), 117.44, 111.42, 55.40, 35.76, -10.60 (d, J = 10 Hz).
31P NMR (203 MHz, C6D6) δP 31.1 (d, J = 14 Hz), 13.5 (br). HRMS (ESI) m/z calc'd for C25H33N2NiO3P2 (M-pyridine) 529.1909. -
- Prepared using a similar procedure as for 27. Complex 28 was isolated as an orange solid (71 mg, 61%).
1H NMR (300 MHz, CD2Cl2) δH 8.44 (s, 8H), 8.13 (br, 1H), 7.76 (m, 4H), 7.73 (m, 2H), 7.42 (m, 1H), 6.85 (m, 2H), 6.78 (t, J = 6.0 Hz, 1H), 6.60 (t, J = 6.0, 2H), 3.41 (br, 4H), 3.18 (s, 6H), 0.74 (br, 24H), -0.89 (d, J = 6.0 Hz, 3H).
13C NMR (125 MHz, C6D6) δC 150.16, 138.01, 135.90 (d, J = 13 Hz), 134.75, 133.57, 133.20, 132.77, 130.51, 129.38, 125.92, 124.92, 123.76, 121.08, 118.52, 117.57 (d, J = 35 Hz), 116.63, 116.00, 111.61, 47.33, 29.69, 24.18, 23.38, 22.34, -10.04 (d, J = 36 Hz).
31P NMR (122 MHz, C6D6) δP 30.0 (d, J = 12 Hz), 14.2 (br). HRMS (ESI) m/z calc'd for C33H49N2NiO3P2 (M-pyridine) 641.2572. -
- Prepared using a similar procedure as for 27. Complex 29 was isolated as a yellow solid (55 mg, 58%). 1H NMR (300 MHz, C6D6) δH 8.41 (br, 8H), 7.67 (br, 4H), 7.42 (m, 1H), 6.89 (m, 2H), 6.81 (m, 2H), 6.71 (m, 3H), 6.48 (m, 7H), 3.19 (septet, J = 6 Hz, 4H), 0.84 (d, J= 6 Hz, 12H), 0.67 (d, J = 6 Hz, 12H), -0.83 (d, J= 9 Hz, 3H).
13C NMR (125 MHz, CD2Cl2) δC 164.33, 161.71 (q, J = 50 Hz), 150.31, 138.45, 135.11, 134.75, 133.31, 131.58, 130.62 (d, J = 1 Hz), 128.84 (q, J = 31 Hz), 127.79, 125.63, 125.16, 123.46, 121.30, 117.41, 112.80 (d, J = 24 Hz), 47.54 (d, J = 5 Hz), 23.22 (d, J = 1 Hz), 22.56 (d, J= 4 Hz), 0.76.
31P NMR (203 MHz, C6D6) δP 29.0 (d, J = 12 Hz) , -8.5 (q, J = 12 Hz). HRMS (ESI) m/z calc'd for C31H41N2NiOP2 (M-pyridine) 653.1984. -
- To a round bottom flask containing magnesium turnings (0.49 g, 20.3 mmol) and THF (50 mL) was added a small crystal of iodine. Then, 1-bromo-2,4-dimethoxybenzene (4.0 g, 18 mmol) as a solution in THF (15 mL) was added slowly over 2 hours. After initiation and stirring for 2 hours the solution was transferred by cannula slowly to a solution of PBr3 (2.94 g, 9.21 mmol) in THF (15 mL) at 0 °C. The solution was stirred overnight at room temperature, then concentrated to 20 mL total volume, brought into an inert atmosphere glovebox, and filtered through Celite. Solvent was removed by vacuum to yield 5.3g of crude bromobis(2,4-dimethoxyphenyl)phosphine which was used in subsequent reactions without further purification.
1H NMR (500 MHz, CDCl3) δ 7.33 (dd, J = 8.5, 3.6 Hz, 1H), 6.52 (dd, J= 8.5, 2.3 Hz, 1H), 6.45 (dd, J = 4.8, 2.3 Hz, 1H), 3.82 (s, 6H).
31P NMR (121 MHz, CDCl3) δP 70.10. - To a solution of N, N, N', N'-tetramethyl phenylphosphonic diamide (0.20 g, 0.94 mmol) in THF (20 mL) was added t-BuLi (0.72 mL, 1.22 mmol, 1.7 M in pentane) at 0 °C and stirred for 30 min. A THF solution of bis(2,4-dimethoxyphenyl)bromophosphine (0.40 g, 1.0 mmol, 6.0 mL solution) was added to the reaction mixture and then warmed slowly to room temperature and stirred for 30 min. The desired PPDA ligand C1a (0.15 g, 30.8 % yield) was isolated as a 2:1 mixture with N, N, N', N'-tetramethyl phenylphosphonic diamide as a white solid by silica gel column chromatography with CH2Cl2/MeOH (95:5) as eluent. This mixture was carried forward without additional purification.
1H NMR (300 MHz, CDCl3) δ 8.24 (m, 1H), 7.42 (m, 1H), 7.34 (m, 1H), 7.10 (m, 1H), 6.49 (m, 4H), 6.39 (m, 2H), 3.81 (s, 6H), 3.68 (s, 6H), 2.55 (d, J = 10 Hz).
31P NMR (121 MHz, CDCl3) δP 30.57 (d, J = 0.9 Hz), 29.64 (s, residual phosphonic diamide starting material), -30.69 (br). - C1a (0.10 g, 0.19 mol) and (h2, h2-cyclooctadi-1,5-ene)(chloro)(methyl)palladium (0.05 g, 0.19 mmol) were weighed into a small vial and then dissolved in dichloromethane (3 mL) at room temperature. The solution was stirred for 10 min. Pentane was layered on top of the solution. After standing overnight, the mother liquor was decanted, the solids were washed with pentane, then dried under vacuum to afford C1b (0.11 g, 84% yield) as a yellow solid. This complex was carried forward without additional purification.
1H NMR (501 MHz, CDCl3) δ 7.50 (m, 3H), 7.37 (m, 2H), 6.44 (br, 5H), 3.82 (s, 6H), 3.55 (b, 6H), 2.57 (br, 12H), 0.42 (d, J= 9.0 Hz, 3H).
31P NMR (203 MHz, CDCl3) δP 33.41 (d, J= 10 Hz), 21.57 (d, J= 9.0 Hz). - C1b (66 mg, 0.074 mmol) and 2,6-lutidine (9 mg, 0.084 mmol) were weighed into a small vial and then dissolved in dichloromethane (5 mL). After dissolution, the solution was added to a flask containing sodium tetrakis[3,5-bis(trifluoromethyl)phenyl]borate (50 mg, 0.074 mmol) cooled to -78 °C. The mixture was slowly warmed to room temperature with vigorous stirring over 30 min. The solids were removed by filtration through Celite, and the filtrate was concentrated to ca. 2 mL and then the solution was diluted with toluene (10 mL). After standing overnight, the precipitate was filtered and washed with pentane, then dried under vacuum to afford 30 (71 mg, 58% yield) as a pale yellow solid.
1H NMR (501 MHz, CDCl3) δ 7.70 (m, 8H, BArF), 7.61 (t, J= 9 Hz, 1H), 7.51 (m, 4H, BArF), 7.47 (m, 3H), 7.38 (m, 1H), 7.15 (m, 2H), 6.96 (m, 1H), 6.58 (m, 5H), 3.85 (s, 6H), 3.56 (br, 6H), 3.05 (br, 6H), 2.52 (s, 6H), 2.24 (b, 12H), -0.10 (d, J= 3 Hz, 3H).
13C NMR (126 MHz, CDCl3) δ 161.81 (dd, J = 99.7, 49.8 Hz), 138.67, 136.38 (d, J = 11.4 Hz), 135.96 (dd, J = 47.5, 8.0 Hz), 134.91, 132.68 (t, J = 10.3 Hz), 132.43, 131.27 (d, J = 18.1 Hz), 130.95 (dd, J = 7.4, 2.5 Hz), 130.25 - 129.86 (m), 129.00 (qdd, J = 31.4, 5.7, 2.8 Hz), 127.91, 125.75, 123.58, 122.87, 121.41, 117.58, 105.44, 98.88, 55.65, 55.12 (d, J = 50.5 Hz), 36.16 (d, J = 170.8 Hz), 26.20 (d, J = 81.6 Hz), -2.62.
31P NMR (203 MHz, CDCl3) δP 33.64 (d, J = 18.0 Hz), 21.59 (d, J = 18.0 Hz).
HRMS (ESI) m/z calc'd for C27H37N2O5P2Pd+ (M-Lutidine) 637.1207, found 637.1198. -
- To a solution of N, N, N', N'-tetramethyl 4-(N, N-dimethylaminophenyl)phosphonic diamide (0. 20 g, 0.78 mmol) in THF (20 mL) was added t-BuLi (0.6 mL, 1.0 mmol, 1.7 M in pentane) at 0 °C and stired for 30 min. A THF solution (5 mL) of bis(2,4-dimethoxyphenyl)bromophosphine (0.33 g, 0.86 mmol) was added to the reaction mixture and then warmed slowly to room temperature then stirred for 30 min. The desired product C2a (0.11 g, 25.1 % yield) was isolated as a 2:1 mixture with residual N, N, N', N'-tetramethyl 4-(N, N-dimethylaminophenyl)phosphonic diamide as a yellow solid after silica gel column chromatography with dichloromethane/MeOH (95:5) as eluent. This mixture was carried forward without further purification.
1H NMR (300 MHz, CDCl3) δ 8.07 (m, 1H), 7.61 (m, 1H), 6.54 (m, 2H), 6.47 (m, 2H), 6.40 (m, 3H), 3.81 (s, 6H), 3.70 (s, 6H), 2.77 (s, 6H), 2.53 (br, 12H).
31P NMR (121 MHz, CDCl3) δ 32.05 (d, J = 1.3 Hz), 31.38 (s, residual phosphonic diamide starting material), -29.42 (br). - C2a (0.07 g, 0.125 mol) and (h2, h2-cyclooctadi-1,5-ene)(chloro)(methyl)palladium (0.033 g, 0.13 mmol) were weighed into a small vial and then dissolved in dichloromethane (3 mL) at room temperature. The solution was stirred for 10 min. Pentane was layered on top of the solution. After standing overnight, the mother liquor was decanted, the solids were washed with pentane, then dried under vacuum to afford C2b (0.075 g, 84% yield) as a yellow solid. This material was carried forward without further purification.
1H NMR (501 MHz, CDCl3) δ 7.63 (br, 1H), 7.35 (m, 1H), 6.72 (m, 2H), 6.56 (m, 2H), 6.44 (m, 3H), 3.82 (s, 6H), 3.68 (br, 6H), 2.79 (s, 6H), 2.61 (d, J= 10 Hz, 12H), 0.48 (d, J= 3 Hz, 3H). 31P NMR (203 MHz, CDCl3) δ 35.18 (d, J = 8.2 Hz), 20.96. - C2b (49 mg, 0.056 mmol) and 2,6-lutidine (7 mg, 0.06 mmol) were weighed into a small vial and then dissolved in dichloromethane (5 mL). After dissolution, the solution was added to a flask containing sodium tetrakis[3,5-bis(trifluoromethyl)phenyl]borate (40 mg, 0.056 mmol) cooled to -78 °C. The mixture was slowly warmed to room temperature with vigorous stirring over 30 min. The solids were removed by filtration through Celite, and the filtrate was concentrated to ca. 2 mL and then the solution was diluted with toluene (10 mL). After standing overnight, the precipitate was filtered and washed with pentane, then dried under vacuum to afford 31 (80 mg, 87% yield) as a yellow solid.
1H NMR (501 MHz, CDCl3) δ 7.70 (m, 8H, BArF), 7.61 (m, 1H), 7.51 (m, 4H, BaRF), 7.15 (m, 2H), 6.72 (m, 3H), 6.48 (br, 3H), 3.84 (s, 6H), 3.64 (br, 6H), 3.06 (s, 6H), 2.81(s, 6H), 2.26 (br, 12H), -0.08 (d, J= 3.5 Hz, 1H).
13C NMR (126 MHz, CDCl3) δ 161.81 (dd, J = 99.7, 49.9 Hz), 151.40 (dd, J = 8.4, 2.4 Hz), 138.53, 136.18 (dd, J = 47.1, 9.6 Hz), 134.91, 134.72 (t, J = 11.5 Hz), 129.74 - 128.46 (m), 127.91, 125.75, 124.35, 123.58, 122.77 (d, J = 3.0 Hz), 121.41, 119.24 (dd, J = 12.1, 5.0 Hz), 117.58, 116.28 (d, J = 18.3 Hz), 114.95 (d, J = 18.3 Hz), 111.88 (d, J = 16.0 Hz), 107.04 (d, J = 59.7 Hz), 105.31, 98.68, 55.63, 55.31, 39.66, 36.16, 26.15, -2.76.
31P NMR (203 MHz, CDCl3) δ 35.27 (d, J= 16.0 Hz), 21.63 (br).
HRMS (ESI) m/z calc'd for C27H37N2O5P2Pd+ (M-Lutidine) 680.16290, found 680.16282. - A 450 mL stainless steel autoclave was dried in an oven at 120 °C, and then allowed to cool inside the dry box. After cooling, toluene (300 mL) and an aliquot of catalyst 27 stock solution (1.35 µmol) was added. The autoclave was then sealed, stirred in a heated oil bath. After the inner temperature reached 95 °C, the autoclave was charged with ethylene (30 bar) and stirred for 15 min. The autoclave exothermed to 117 °C. The reaction was then quenched by addition of MeOH. The mixture was filtered and washed with MeOH. The solids were dried under vacuum at 80 °C overnight to afford 19.20 g polyethylene. The molecular weight and polydispersity were determined by size exclusion chromatography. The extent of branching in the polymer backbone was determined by 1H NMR spectroscopy.
Catalyst Tmax (°C)a yield (g) Activity[× 10-6 g (mol Ni)-1 h-1] TOF (× 10-6 h-1) M w (× 10-3 g mol-1)b Ð (M w/ Mn )b Me brc 26d 11.4 27 0.98 170 2.6 2.2 27 117 19.2 57 2.0 21 1.7 1.5 28 109 11.2 33 1.2 170 2.2 n.d.e 29 100 3.1 9.3 0.33 99 1.6 n.d.e aMaximum temperature during polymerization due to reaction exotherm. bAbsolute molecular weight and polydispersity determined by GPC analysis with triple detection. cMethyl branches per 1000 carbons as determined by 1H or quantitative 13C NMR spectroscopy. dConditions: 26 (1.25 mmol) and C2H4 (30 bar) were stirred in toluene (0.2 L) at 100 °C for 20 min. eNot determined. - A 450 mL stainless steel autoclave was dried in an oven at 120 °C, and then allowed to cool inside the dry box. After cooling, toluene (300 mL), an aliquot of catalyst 27 stock solution (1.35 µmol) and MEHQ (0.25 g, 1500 equiv.) was added. The autoclave was then sealed, stirred in a heated oil bath. After the inner temperature reached 100 °C, the autoclave was charged with ethylene (30 bar) and stirred for 15 min. The reaction was then quenched by addition of MeOH. The mixture was filtered and washed with MeOH. The solids were dried under vacuum at 80 °C overnight to afford 10.42 g polyethylene. The molecular weight and polydispersity were determined by size exclusion chromatography.
Additive Equiv Yield (g) Av TOF [mol (mol Ni)-1 h-1] krel M w (× 10-3 g mol-1)a Ð (M w/M n )a None - 18.6 2,000,000 1 26 1.7 MEHQ 1500 18.6 2,000,000 1 23 1.5 Et2O 1500 10.4 1,100,000 0.6 26 1.7 Ethyl acetate 1500 17.9 1,900,000 1 24 1.7 H2O 1250 11.4 1,200,000 0.6 26 1.7 NEt3 1500 0.07 7,400 0.004 - - O2 (1 atm) 0 0 0 - - aAbsolute molecular weight and polydispersity determined by GPC analysis with triple detection. - As provided in this Example 8, polymerization continued in the presence of the functional additives known to disrupt and/or preclude ethylene polymerization with prior transition metal catalysts.
- A 450 mL stainless steel autoclave was dried in an oven at 120 °C, and then allowed to cool inside the dry box. After cooling, toluene (300 mL) and an aliquot of catalyst 27 stock solution (1.35 µmol) was added. The autoclave was then sealed, stirred in a heated oil bath. After the inner temperature reached 100 °C, the autoclave was charged with ethylene (3.5 bar) and stirred for 15 min. The reaction was then quenched by addition of MeOH. The mixture was filtered and washed with MeOH. The solids were dried under vacuum at 80 °C overnight to afford polyethylene. The molecular weight and polydispersity were determined by size exclusion chromatography.
Entry time (h) yield (g) Productivity [kg (mol Ni-1)] TOF (× 10-3 h-1) M w (× 10-3 g mol-1)a Ð (Mw /M n)a 1 0.25 0.90 670 95 15 2.0 2 0.5 1.4 1000 76 16 1.7 3 1 3.1 2300 83 16 1.8 4 1.5 3.9 2900 68 17 1.6 5 2 4.3 3200 57 120 1.8 aAbsolute molecular weight and polydispersity determined by GPC analysis with triple detection. - A 25 mL stainless steel autoclave was dried in an oven at 120 °C, and then allowed to cool inside the dry box. After cooling, an aliquot of catalyst 27 stock solution (10 µmol) and butyl vinyl ether (1.94 mL, 15 mmol) were diluted with toluene to 15 mL. The autoclave was then sealed, stirred in a heated oil bath. The autoclave was charged with ethylene (30 bar), heated to 100 °C and stirred for 12 hours. The reaction was then quenched by addition of MeOH. The mixture was filtered and washed with MeOH. The solids were rinsed with chloroform to remove any poly(butyl vinyl ether) and dried under vacuum at 80 °C overnight to afford 0.65 g polyolefin. The molecular weight and polydispersity were determined by size exclusion chromatography. The percent incorporation of functional monomer in the polymer backbone was determined by 1H NMR spectroscopy.
Catalyst yield (g) Activity [× 10-3 g (mol Ni)-1 h-1] M w (× 10-3 g mol-1)a Ð (Mw /Mn )a % incorp.b 27 0.65 5.4 9.4 2.2 0.05 aAbsolute molecular weight and polydispersity determined by GPC analysis with triple detection. bMethyl branches per 1000 carbons as determined by quantitative 13C NMR spectroscopy. - A 25 mL stainless steel autoclave was dried in an oven at 120 °C, and then allowed to cool inside the dry box. After cooling, toluene (10 mL) and 30 (1.25 µmol, 2.0 mg) was added. The autoclave was then sealed and stirred in a heated oil bath. After the inner temperature reached 100 °C, the autoclave was then charged with ethylene (30 bar) and stirred for 15 min. The reaction was then quenched by addition of MeOH. The mixture was filtered and washed with MeOH. The solids were dried under vacuum at 100 °C overnight to afford 0.52 g white solid. The molecular weight and polydispersity were determined by size exclusion chromatography. The extent of branching in the polymer backbone was determined by 1H-NMR spectroscopy. The same procedure was repeated for 31.
- A 25 mL stainless steel autoclave was dried in an oven at 120 °C, and then allowed to cool inside the dry box. After cooling, toluene (12 mL) 30 (10.5 µmol, 17.0 mg) and methyl acrylate (3mL, 33.1mmol) was added. The autoclave was then sealed and stirred in a heated oil bath. After the inner temperature reached 100 °C, the autoclave was then charged with ethylene (30 bar) and stirred for 12 hrs. The reaction was then quenched by addition of MeOH. The mixture was filtered and washed with MeOH. The polymer was redissolved in 10 mL toluene and precipitated again by the addition of MeOH. The solids were dried under vacuum at 100 °C overnight to afford 1.03 g white solid. The molecular weight and polydispersity were determined by size exclusion chromatography. The comonomer incorporation was determined by 1H-NMR spectroscopy. The same procedure was repeated for 31.
- Various embodiments of the invention have been described in fulfillment of the various objectives of the invention. It should be recognized that these embodiments are merely illustrative of the principles of the present invention.
Claims (13)
- A method of polymerization comprising:providing a reaction mixture including olefin monomer, polar monomer and transition metal complex of Formula (II):
wherein M is a transition metal, A is selected from the group consisting of alkyl, alkenyl, aryl and heteroaryl, and wherein R1, R2, R3, R4, R5 and R6 are independently selected from the group consisting of alkyl, heteroalkyl, cycloalkyl, heterocycloalkyl, aryl, heteroaryl, alkyl-aryl and alkyl-heteroaryl, wherein R1 and R2 may optionally form a ring structure and any combination of R3, R4, R5 and/or R6 may optionally form a ring structure and wherein R7 is selected from the group consisting of alkyl and aryl and R8 is selected from the group consisting of amine, heteroaryl, monophosphine, halo and sulfoxide and wherein X- is a non-coordinating counter anion; andcopolymerizing the olefin monomer with the polar monomer in the presence of the transition metal complex. - The method of claim 1, wherein the polar monomer is selected from the group consisting of acrylic acid, alkyl acrylic acids, alkyl acrylates, acetates, acrylamide, vinyl ethers and/or acrylonitrile.
- The method of claim 2, wherein the olefin monomer is ethylene or propylene.
- The method of claim 1, wherein M is palladium.
- The method of claim 1, wherein M is nickel.
- The method of claim 1, wherein copolymer resulting from the copolymerization has molecular weight (Mw) of at least 5,000 Da.
- The method of claim 1, wherein copolymer resulting from the copolymerization has molecular weight (Mw) of at least 10,000-200,000 Da.
- The method of claim 1, wherein at least 50 percent of the polar monomer is incorporated in-chain.
- The method of claim 1, wherein at least 90 percent of the polar monomer is incorporated in-chain.
- The method of claim 1, wherein the polar monomer is exclusively incorporated in-chain.
- The method of claim 1, wherein M is palladium or nickel, A and R1-R2 are independently aryl, R3-R6 are independently alkyl, R7 is selected from alkyl and aryl and R8 is selected from the group consisting of heteroaryl, halo and sulfoxide.
- The method of claim 1, wherein 3-15 mol.% polar monomer is incorporated into the copolymer.
- The method of claim 8, wherein 5-15 mol.% polar monomer is incorporated into the copolymer.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US201462018263P | 2014-06-27 | 2014-06-27 | |
| PCT/US2015/038104 WO2015200849A2 (en) | 2014-06-27 | 2015-06-26 | Transition metal catalysts for olefin polymerization |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| EP3160975A2 EP3160975A2 (en) | 2017-05-03 |
| EP3160975A4 EP3160975A4 (en) | 2018-05-16 |
| EP3160975B1 true EP3160975B1 (en) | 2019-10-09 |
Family
ID=54938960
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP15811109.6A Active EP3160975B1 (en) | 2014-06-27 | 2015-06-26 | Transition metal catalysts for olefin polymerization |
Country Status (3)
| Country | Link |
|---|---|
| US (2) | US10266623B2 (en) |
| EP (1) | EP3160975B1 (en) |
| WO (1) | WO2015200849A2 (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105061505A (en) * | 2015-09-16 | 2015-11-18 | 中国科学技术大学 | Catalyst ligand, catalyst, and preparation methods and application thereof |
| EP3786196B1 (en) * | 2018-04-25 | 2024-05-08 | The University of Tokyo | Method for producing copolymer of allyl monomer having polar group |
| WO2020009846A2 (en) * | 2018-07-03 | 2020-01-09 | University Of Houston System | Heterobimetallic catalysts and site-differentiated ligands for preparation thereof |
| CN111116810B (en) * | 2018-10-31 | 2023-01-17 | 中国石油化工股份有限公司 | Preparation method of olefin-olefin alcohol copolymer |
| CN113019461B (en) * | 2021-03-17 | 2022-07-12 | 天津科技大学 | Catalyst system for selective oligomerization of ethylene, reaction method and application thereof |
| WO2024025606A1 (en) * | 2022-07-27 | 2024-02-01 | University Of Houston System | Nickel catalysts with two alkali ions for homopolymerization and copolymerization |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4098756A (en) * | 1976-07-12 | 1978-07-04 | Allied Chemical Corporation | Fluoropolymer primer compositions |
| EP3190120B1 (en) * | 2012-05-11 | 2021-11-17 | The University Of Tokyo | Catalyst for synthesizing polyolefins |
-
2015
- 2015-06-26 WO PCT/US2015/038104 patent/WO2015200849A2/en not_active Ceased
- 2015-06-26 EP EP15811109.6A patent/EP3160975B1/en active Active
- 2015-06-26 US US15/322,347 patent/US10266623B2/en active Active
-
2019
- 2019-04-17 US US16/387,100 patent/US11021554B2/en active Active
Non-Patent Citations (1)
| Title |
|---|
| None * |
Also Published As
| Publication number | Publication date |
|---|---|
| US20170137549A1 (en) | 2017-05-18 |
| WO2015200849A3 (en) | 2016-04-07 |
| EP3160975A4 (en) | 2018-05-16 |
| WO2015200849A2 (en) | 2015-12-30 |
| EP3160975A2 (en) | 2017-05-03 |
| US11021554B2 (en) | 2021-06-01 |
| US10266623B2 (en) | 2019-04-23 |
| US20190338058A1 (en) | 2019-11-07 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US11021554B2 (en) | Transition metal catalysts for olefin polymerization | |
| Chen et al. | Promoting Ethylene (co) Polymerization in Aliphatic Hydrocarbon Solvents Using tert‐Butyl Substituted Nickel Catalysts | |
| EP3190120B1 (en) | Catalyst for synthesizing polyolefins | |
| JPWO2012014844A1 (en) | Catalyst for polythiophene polymerization and method for producing poly (substituted thiophene) | |
| US11352453B2 (en) | Catalyst for olefin polymerization and production method for polar group-containing olefin-based polymers | |
| US8889805B2 (en) | Carboxylate metal complex and catalyst for olefin polymerization | |
| JPWO2016067776A1 (en) | Method for producing polar group-containing olefin polymer | |
| CN105061505A (en) | Catalyst ligand, catalyst, and preparation methods and application thereof | |
| KR101442001B1 (en) | Method for producing polar group-containing olefin copolymers | |
| EP1964857B1 (en) | Polymerization of acyclic aliphatic olefins | |
| KR101997692B1 (en) | N-Heterocyclic carbene metallocene compounds and method for preparing the same | |
| JP2016084437A (en) | Method for producing polar group-containing olefin polymer | |
| US20070287847A1 (en) | Ligand Synthesis | |
| KR102734118B1 (en) | Process for preparing indene derivative, process for preparing metallocene catalyst, process for olefin polymer using the same | |
| JP7705643B2 (en) | Catalyst for olefin polymerization and method for producing olefin polymer | |
| JP5585916B2 (en) | Process for producing polythiophenes and novel thiophene monomer | |
| WO2019207969A1 (en) | Method for producing copolymer of allyl monomer having polar group | |
| JP2017088883A (en) | Polar group-containing propylene olefin copolymer and manufacturing method therefor | |
| Zhu | Zwitterionic Nickel Catalysts for Carbonylative Polymerization of Olefins | |
| Xie et al. | Synthesis, structure characterization and catalytic activity of lanthanide complexes containing an ansa carbonous‐bridged cyclopentadienyl—thienyl ligand | |
| US7728091B2 (en) | Polymerization of phosphaalkenes | |
| KR20220039376A (en) | Manufacturing method for polymer |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE INTERNATIONAL PUBLICATION HAS BEEN MADE |
|
| PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
| STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: REQUEST FOR EXAMINATION WAS MADE |
|
| 17P | Request for examination filed |
Effective date: 20161219 |
|
| AK | Designated contracting states |
Kind code of ref document: A2 Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR |
|
| AX | Request for extension of the european patent |
Extension state: BA ME |
|
| DAV | Request for validation of the european patent (deleted) | ||
| DAX | Request for extension of the european patent (deleted) | ||
| RIC1 | Information provided on ipc code assigned before grant |
Ipc: C08F 4/70 20060101ALI20180115BHEP Ipc: C07F 9/53 20060101AFI20180115BHEP Ipc: C07F 19/00 20060101ALI20180115BHEP Ipc: C08F 220/14 20060101ALI20180115BHEP Ipc: C07F 15/00 20060101ALI20180115BHEP Ipc: C08F 210/02 20060101ALI20180115BHEP |
|
| A4 | Supplementary search report drawn up and despatched |
Effective date: 20180416 |
|
| RIC1 | Information provided on ipc code assigned before grant |
Ipc: C08F 220/14 20060101ALI20180410BHEP Ipc: C07F 9/53 20060101AFI20180410BHEP Ipc: C07F 15/00 20060101ALI20180410BHEP Ipc: C08F 4/70 20060101ALI20180410BHEP Ipc: C07F 19/00 20060101ALI20180410BHEP Ipc: C08F 210/02 20060101ALI20180410BHEP |
|
| STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: EXAMINATION IS IN PROGRESS |
|
| 17Q | First examination report despatched |
Effective date: 20180718 |
|
| GRAP | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOSNIGR1 |
|
| STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: GRANT OF PATENT IS INTENDED |
|
| INTG | Intention to grant announced |
Effective date: 20190301 |
|
| GRAS | Grant fee paid |
Free format text: ORIGINAL CODE: EPIDOSNIGR3 |
|
| GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
| STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE PATENT HAS BEEN GRANTED |
|
| AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR |
|
| REG | Reference to a national code |
Ref country code: GB Ref legal event code: FG4D |
|
| REG | Reference to a national code |
Ref country code: CH Ref legal event code: EP |
|
| REG | Reference to a national code |
Ref country code: IE Ref legal event code: FG4D |
|
| REG | Reference to a national code |
Ref country code: DE Ref legal event code: R096 Ref document number: 602015039584 Country of ref document: DE |
|
| REG | Reference to a national code |
Ref country code: AT Ref legal event code: REF Ref document number: 1188672 Country of ref document: AT Kind code of ref document: T Effective date: 20191115 |
|
| REG | Reference to a national code |
Ref country code: NL Ref legal event code: MP Effective date: 20191009 |
|
| REG | Reference to a national code |
Ref country code: LT Ref legal event code: MG4D |
|
| REG | Reference to a national code |
Ref country code: AT Ref legal event code: MK05 Ref document number: 1188672 Country of ref document: AT Kind code of ref document: T Effective date: 20191009 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: PT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200210 Ref country code: ES Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191009 Ref country code: GR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200110 Ref country code: NL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191009 Ref country code: AT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191009 Ref country code: NO Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200109 Ref country code: BG Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200109 Ref country code: PL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191009 Ref country code: FI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191009 Ref country code: LT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191009 Ref country code: SE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191009 Ref country code: LV Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191009 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: HR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191009 Ref country code: RS Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191009 Ref country code: IS Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200224 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: AL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191009 |
|
| REG | Reference to a national code |
Ref country code: DE Ref legal event code: R097 Ref document number: 602015039584 Country of ref document: DE |
|
| PG2D | Information on lapse in contracting state deleted |
Ref country code: IS |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: RO Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191009 Ref country code: CZ Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191009 Ref country code: DK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191009 Ref country code: EE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191009 Ref country code: IS Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20200209 |
|
| PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
| STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SM Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191009 Ref country code: SK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191009 Ref country code: IT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191009 |
|
| 26N | No opposition filed |
Effective date: 20200710 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191009 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: MC Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191009 |
|
| REG | Reference to a national code |
Ref country code: CH Ref legal event code: PL |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LU Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20200626 |
|
| REG | Reference to a national code |
Ref country code: BE Ref legal event code: MM Effective date: 20200630 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20200626 Ref country code: CH Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20200630 Ref country code: FR Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20200630 Ref country code: LI Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20200630 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: BE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20200630 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: TR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191009 Ref country code: MT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191009 Ref country code: CY Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191009 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: MK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20191009 |
|
| PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GB Payment date: 20250627 Year of fee payment: 11 |
|
| PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 20250729 Year of fee payment: 11 |